http://rdf.ncbi.nlm.nih.gov/pubchem/patent/KR-101688894-B1

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filingDate 2016-08-08-04:00^^<http://www.w3.org/2001/XMLSchema#date>
grantDate 2016-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_8e94ac1fa4484683dddd740b0ccf3cc2
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publicationDate 2016-12-23-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-101688894-B1
titleOfInvention Using high temperature catalytic combustion burners
abstract A burner using a high temperature combustion catalyst is disclosed. A burner using the disclosed hot combustion catalyst comprises a mixing and dispensing unit for mixing and dispensing the supplied fuel gas and air; A combustion catalyst unit for generating heat by a catalytic combustion reaction with the fuel gas supplied from the mixing and dispensing unit; And a premixing chamber for premixing the combustion gas entering the combustion catalyst unit while connecting the mixing and distributing unit and the combustion catalyst unit, wherein the combustion catalyst unit comprises: A front and rear open housing having a chamber; A perforated plate installed on the front and rear surfaces of the housing to allow the fuel gas to pass forward from the rear of the housing; A pellet type combustion catalyst filled in the chamber of the housing; And a heat source means for generating a heat source for catalytic combustion of the combustion catalyst, wherein the high temperature combustion catalyst comprises: preparing a metal precursor solution containing a nitrate transition metal, an alkaline earth metal nitrate, and an aluminum nitrate; Preparing a precipitation solution; Mixing the metal precursor solution and the precipitating solution to prepare a mixed solution; Raising the temperature of the mixed solution to 90 to 100 占 폚, and maintaining the mixture solution for 10 to 48 hours; Separating the precipitate slurry formed by the precipitation reaction from the mixed solution by filtration; Washing the precipitate slurry with water; Drying to remove moisture in the washed precipitate slurry; And calcining the dried precipitate slurry at 1,000 to 1,500 DEG C to remove moisture remaining in the dried precipitate slurry.
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